US2123536A - Process for the manufacture of multicellular glass - Google Patents
Process for the manufacture of multicellular glass Download PDFInfo
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- US2123536A US2123536A US23709A US2370935A US2123536A US 2123536 A US2123536 A US 2123536A US 23709 A US23709 A US 23709A US 2370935 A US2370935 A US 2370935A US 2123536 A US2123536 A US 2123536A
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- glass
- mixture
- vitreous
- heating
- comminuted
- Prior art date
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- 239000011521 glass Substances 0.000 title description 67
- 238000000034 method Methods 0.000 title description 22
- 238000004519 manufacturing process Methods 0.000 title description 16
- 239000000126 substance Substances 0.000 description 35
- 239000007789 gas Substances 0.000 description 27
- 239000000203 mixture Substances 0.000 description 27
- 238000010438 heat treatment Methods 0.000 description 23
- 238000001816 cooling Methods 0.000 description 10
- 239000002245 particle Substances 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 8
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 7
- 229910021653 sulphate ion Inorganic materials 0.000 description 7
- 239000003245 coal Substances 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 4
- 239000003638 chemical reducing agent Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 239000005373 porous glass Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 229920001353 Dextrin Polymers 0.000 description 1
- 101100348017 Drosophila melanogaster Nazo gene Proteins 0.000 description 1
- 239000001828 Gelatine Substances 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- GPUADMRJQVPIAS-QCVDVZFFSA-M cerivastatin sodium Chemical compound [Na+].COCC1=C(C(C)C)N=C(C(C)C)C(\C=C\[C@@H](O)C[C@@H](O)CC([O-])=O)=C1C1=CC=C(F)C=C1 GPUADMRJQVPIAS-QCVDVZFFSA-M 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- FYGDTMLNYKFZSV-MRCIVHHJSA-N dextrin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)OC1O[C@@H]1[C@@H](CO)OC(O[C@@H]2[C@H](O[C@H](O)[C@H](O)[C@H]2O)CO)[C@H](O)[C@H]1O FYGDTMLNYKFZSV-MRCIVHHJSA-N 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- HCWCAKKEBCNQJP-UHFFFAOYSA-N magnesium orthosilicate Chemical compound [Mg+2].[Mg+2].[O-][Si]([O-])([O-])[O-] HCWCAKKEBCNQJP-UHFFFAOYSA-N 0.000 description 1
- 239000000391 magnesium silicate Substances 0.000 description 1
- 229910052919 magnesium silicate Inorganic materials 0.000 description 1
- 235000019792 magnesium silicate Nutrition 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 235000012222 talc Nutrition 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C11/00—Multi-cellular glass ; Porous or hollow glass or glass particles
- C03C11/007—Foam glass, e.g. obtained by incorporating a blowing agent and heating
Definitions
- This invention relates to a process 'for' the manufacture of sponge-like or multicellular glass and refers more particularly to a process of treating a glass-containing mixture in such manner that a porous vitreous product is obtained, -which contains a plurality of cells which are separated one from the other.
- An object of the present invention is the provision of a simple and eilicient method of manufacturing multicellular glass, the structure of which will be more regular and uniform than that of the glass manufactured by any other methods.
- Another object is the provision of multicellular glass the cells of which are distributed very evenly throughout the entire mass of the glass.
- a further object of this invention is the provision of porous glass which is extremely light and the density of which is often as low as 0.35.
- the above and other objects of the present invention may be realized by mixing comminuted glass, or a mixture of fritted and ground vitreous substances, with one or more pulverized substances capable of developing gases or vapors at a certain temperature, and then by heating this mixture to this temperature, which should be one. at which the glass particles become soft and are joined one to the other simply by contact.
- the formation of. gases or vapors may be caused either by a chemical reaction taking-place between at least one of these pulverized substances, and the glass, or by a reaction taking place between the pulverized substances, or mere- 1y by a decomposition of the gas developing substances.
- the mass vitrified in this manner is cooled after the gases or vapors developed therein have increased the volume of the mass to the desired extent in order that it may have a certain predetermined apparent density.
- First example A mixture of pulverized reducing substances, carbon or carbon-containing substances, carbides, particularly silicium carbide, silicium and ferro sllicons, with a suitable amount of comminuted glass, preferably, aluminous glass which contains an alkaline sulphate or alkaline earth i" sulphate is placed into a mold. To this mixture may be added, if necessary, a small quantity of an adhesive substance such as gelatine, dextrine,
- the entire mixture is heated to a tem- 55 perature at which the glass becomes plastic or soft, that is, to a temperature of about 800: C. or 900 C.
- the reducing substances decompose the sulphate and give up bubbles of sulphurous gas which is often mixed with the carbonic gas.
- the bubbles remain within the mixture after it has become solid due -to the great viscosity of glass.
- the glass containing sulphate may be prepared by means of a vitrlflable mixture, the fusion of which is stopped before the refining process is commenced.
- the glass may be composed of the following ingredients:
- Glass of the above type may be mixed with silicium carbide (popularly known under the trade name Carborundum) in a proportion of 70% of' the glass, to 30% of silicium carbide.
- silicium carbide popularly known under the trade name Carborundum
- the apparent density .of which is as low as 0.35.
- the vitreous mixture may contain the following ingredients:
- Comminuted glass 90' Silica white 3 Soda sulphate 6 Coal 1 Third example Glass particles are mixed with talcum or hydrated magnesium silicate. 1 The mixture is heated until it reaches a temperature ofabout 850 C. At this temperature the hydrated magnesiumsillcate loses its hydration water which is transformed into steam. This steam swells the glass which has become plastic under the influence of heat and forms cells in the glass.
- Pulverized glass is mixed with pulverized coal. This mixture is projected into a mold heated to a temperature from 800-to 900 C. "The mixture swells and fills the mold. In practice, 0.5 part of vegetable coal mixedwith 100 parts of glass are suijlicient to produce multicellular glass of which apparent density is 0.40.
- the comminuted glass may be replaced by vitrifiable substances which have not been vitrified as yet,
- a multicellular glass may be obtained, the structure of which is much more regular than that of the sponge-like glass produced by any other methods. This is caused by the very uniform and even distribution of the gas and vapor bubbles throughout theentire vitreous mass. Furthermore, due to the very uniform distribution of the gas bubbles, the product obtained by the described methods is extremely light. It's
- the process for the manufacture of multioellular glass which comprises mirdng solid comminuted vitreous substances with a pulverized substance capable of giving up gases, heating the mixture to a temperature at which the particles of the comminuted substance become soft and are joined to each other by mere contact, the second-mentioned substance being capable of producing gases at said temperature, interrupting the heating when the gases developed within the vitreous mass increase the volume thereof to the desired extent whereby cells are formed which are separated one from the other, and then cooling said mass, whereby multicellular glass of predetermined apparent-density is produced.
- the process for the manufacture of multicellular glass which comprises mixing solid comminuted glass with pulverized substances capable of producing gases within a certain range of temperatures, heating the mixture to atemperature at which the particles of the comminuted glass become soft and are joined to each other by mere contact, 'the last-mentionedtemperature being within the first-mentioned.range of temperatures, interrupting the heating when the gases developed within the glassy mass increase the volume thereof to the desired extent whereby cells are formed which "are separated one from the other, and then cooling said mass. whereby multicellular glass of predetermined apparent density is produced.
- the process for the manufacture of multicellular glass which comprises mixing comminuted glass with a pulverized substance capable of ch ically reacting with said glass within a certa n range of temperatures, a gas being produced in the course of said reaction, heating the-mixture to a temperature at which the particles of the comminuted glass become soft and are joined to each other by mere contact, the last mentioned temperature being within the first mentioned range of temperatures, interrupting the heating when the gas developed within the glassy mass increases the volume thereof to the desired extent whereby cells are formed which are separated one from the other, and then cooling said mass, whereby multicellular glass of predetermined apparent density is produced. 4.
- the process for the manufacture of multicellular glass which comprises mixing comminuted fritted vitrifiable substances with at least one pulverized substance capable'of chemically reacting with said vitrifirble substances within a certain range of temperatures, a gas being produced in the course of said reaction, heating the mixture to a temperature at which the particles of the vitriflable substances become soft and are joined to each other by mere contact, the last mentioned temperature being within the first-mentioned range of temperatures, the heating being continued until the mixture is vitrified, interrupting the heating when the gases developed within the vitrified massincr'ease the volume thereof to the desired extent whereby cells are formed which are separated one from the other, and then cooling sa'id mass, whereby multicellular glass of predetermined apparent density is produced.
- the process for the manufacture of multicellul'ar glass which comprises mixing a comminuted vitreous substance with pulverized substances capable of reacting with each other within a certain range of temperatures and of developing a gas in the course of this reaction, heating the mixture to a temperature at which the particles of the comminuted vitreous substance become soft and are joined to each other by mere contact, the last-mentioned temperature being within the first mentioned range of tempera-' tures, interrupting the heating when the gas developed within the vitreous massincreases the volume thereof to the desired extent whereby cells are formed which are separated one from the other, and then cooling'said mass, whereby multicellular glass of predetermined apparent density is produced.
- the process for the manufacture of multicellular glass which comprises 'mixing a solid comminuted vitreous substance with a pulverized substance capable of giving up a gaseous fluid within a certain range of temperatures, heating the mixture to a temperature at which the particles of the comminuted vitreous substance become soft and are joined to each other by mere contact.
- the last-mentioned temperature being within the first-mentioned range of temperatures, interrupting the heating when the gaseous fluid developed within the vitreous mass increases the volume thereof to the desired extent whereby cells are formed whichare separated one from the other, andthen cooling said mass, whereby multicellular glass of predetermined apparent density is produced.
- the process of manufacturing multicellular tarts glass which comprises mixing comminuted glass containing alkaline sulphates with a. reducing substance capable of reacting with said glass lular glass of predetermined apparent densityis produced.
- the process of manufacturing multicellular glass which comprises mixing a comminuted vitreous substance containing a sulphate with a carbonaceous reducing substance capable of reacting with said vitreous substance within a certain range of temperatures, at least one gas being produced'in the course of this reaction, heating the mixture to the softening temperature of said vitreous substance, said softening temperature being within said range of temperatures, interrupting the heating when the bubbles of said gas within the vitreous mass increase the volume thereof to the desired extent wherebycells are formed which are separated one from the other, and thencooling said mass, whereby multicelluiar glass of predetermined apparent density is produced.
- the process of manufacturing multiceliular glass which comprises mixing a comminuted vitreous substance with a carbonaceous reducing substance capable of reacting with said vitreous substance within a certain range of temperatures, at least one gas being produced in the course of this reaction, heating the mixture to the softening temperature of said vitreous sub stance, said softening temperature being within said range of temperatures, interrupting the heating when the bubbles of said gas within the vitreous mass increase the volume thereof to the desired extent whereby cells-are formed" which are separated one fromthe other, and then cooling said mass, whereby multicellular glass of predetermined apparent density is produced.
- the process of manufacturing multicelluiar glass which comprises mixing a comminuted vitreous substance with a mixture containing finely pulverized silica, soda sulphate and coal, heating the mixture to the softening temperature of said vitreous substance, said softening temperature being within the range of temperatures at which the mixture develops gas, interrupting the heating when the bubbles of said gas" within the vitreous mass increase the volume thereof to the desired extent whereby cells are formed which are separated one from the other, and then cooling said mass, whereby multicellular glass of predetermined apparent density is produced.
- The'process of manufacturing multicellular glass which comprises mixing a solid comminuted vitreous substance with pulverized coal, projecting this mixture into a mold heated to the range of temperatures at which the particles.
Description
such as,
Patented July 12, 1938 UNITED STATES PATENT orricl-z PROCESS FOR THE MANUFACTURE OF MULTICELLULAR GLASS No Drawing. Application May 27, 1935, Serial No. 23,709. In France May 28, 1934 12 Claims.
This invention relates to a process 'for' the manufacture of sponge-like or multicellular glass and refers more particularly to a process of treating a glass-containing mixture in such manner that a porous vitreous product is obtained, -which contains a plurality of cells which are separated one from the other.
An object of the present invention is the provision of a simple and eilicient method of manufacturing multicellular glass, the structure of which will be more regular and uniform than that of the glass manufactured by any other methods.
Another object is the provision of multicellular glass the cells of which are distributed very evenly throughout the entire mass of the glass.
A further object of this invention is the provision of porous glass which is extremely light and the density of which is often as low as 0.35.
The above and other objects of the present invention, may be realized by mixing comminuted glass, or a mixture of fritted and ground vitreous substances, with one or more pulverized substances capable of developing gases or vapors at a certain temperature, and then by heating this mixture to this temperature, which should be one. at which the glass particles become soft and are joined one to the other simply by contact. The formation of. gases or vapors may be caused either by a chemical reaction taking-place between at least one of these pulverized substances, and the glass, or by a reaction taking place between the pulverized substances, or mere- 1y by a decomposition of the gas developing substances. The mass vitrified in this manner is cooled after the gases or vapors developed therein have increased the volume of the mass to the desired extent in order that it may have a certain predetermined apparent density.
Several methods of carrying out this invention will be described now by way of example:
-. First example A mixture of pulverized reducing substances, carbon or carbon-containing substances, carbides, particularly silicium carbide, silicium and ferro sllicons, with a suitable amount of comminuted glass, preferably, aluminous glass which contains an alkaline sulphate or alkaline earth i" sulphate is placed into a mold. To this mixture may be added, if necessary, a small quantity of an adhesive substance such as gelatine, dextrine,
or soda silicate.
Then the entire mixture is heated to a tem- 55 perature at which the glass becomes plastic or soft, that is, to a temperature of about 800: C. or 900 C.
The reducing substances decompose the sulphate and give up bubbles of sulphurous gas which is often mixed with the carbonic gas. The bubbles remain within the mixture after it has become solid due -to the great viscosity of glass.
The glass containing sulphate may be prepared by means of a vitrlflable mixture, the fusion of which is stopped before the refining process is commenced.
The glass may be composed of the following ingredients:
SiO: 70.00 or 72.70 NazO 14.24 14.30 0:30 4.90 7.60 MgO 3.00 A1203 7.00 2.00 B203 3.55
SO; 0.30 I 0.40
Glass of the above type may be mixed with silicium carbide (popularly known under the trade name Carborundum) in a proportion of 70% of' the glass, to 30% of silicium carbide. When the total mixture is heated in the abovedescribed manner, a porous glass is produced, the apparent density .of which is as low as 0.35.
Second example The vitreous mixture may contain the following ingredients:
Comminuted glass 90' Silica white 3 Soda sulphate 6 Coal 1 Third example Glass particles are mixed with talcum or hydrated magnesium silicate. 1 The mixture is heated until it reaches a temperature ofabout 850 C. At this temperature the hydrated magnesiumsillcate loses its hydration water which is transformed into steam. This steam swells the glass which has become plastic under the influence of heat and forms cells in the glass.
Fourth example the bubbles of air and .steam are liberated andexpand forming pores within the glass which has become plastic under the influence of heat.
Fifth example Pulverized glass is mixed with pulverized coal. This mixture is projected into a mold heated to a temperature from 800-to 900 C. "The mixture swells and fills the mold. In practice, 0.5 part of vegetable coal mixedwith 100 parts of glass are suijlicient to produce multicellular glass of which apparent density is 0.40.
In order to avoid that the ,glass sticks to the mold it has been found useful to use a mold made of graphite.
In all of the above described examples the comminuted glass may be replaced by vitrifiable substances which have not been vitrified as yet,
., but which have been simply fritted at a temperature of about 700 C. to 800 C.,and then granulated.
Through the use of the described methods a multicellular glass may be obtained, the structure of which is much more regular than that of the sponge-like glass produced by any other methods. This is caused by the very uniform and even distribution of the gas and vapor bubbles throughout theentire vitreous mass. Furthermore, due to the very uniform distribution of the gas bubbles, the product obtained by the described methods is extremely light. It'
does not contain any parts which are more or less devoid of cells. Finally, due to the very small apparent density of the article, its surfaces can be treated much more conveniently by any mechanical utensils or machines generally used for shaping glass.
What is claimed is: v
1. The process for the manufacture of multioellular glass, which comprises mirdng solid comminuted vitreous substances with a pulverized substance capable of giving up gases, heating the mixture to a temperature at which the particles of the comminuted substance become soft and are joined to each other by mere contact, the second-mentioned substance being capable of producing gases at said temperature, interrupting the heating when the gases developed within the vitreous mass increase the volume thereof to the desired extent whereby cells are formed which are separated one from the other, and then cooling said mass, whereby multicellular glass of predetermined apparent-density is produced.
2. The process for the manufacture of multicellular glass, which comprises mixing solid comminuted glass with pulverized substances capable of producing gases within a certain range of temperatures, heating the mixture to atemperature at which the particles of the comminuted glass become soft and are joined to each other by mere contact, 'the last-mentionedtemperature being within the first-mentioned.range of temperatures, interrupting the heating when the gases developed within the glassy mass increase the volume thereof to the desired extent whereby cells are formed which "are separated one from the other, and then cooling said mass. whereby multicellular glass of predetermined apparent density is produced.
3. The process for the manufacture of multicellular glass, which comprises mixing comminuted glass with a pulverized substance capable of ch ically reacting with said glass within a certa n range of temperatures, a gas being produced in the course of said reaction, heating the-mixture to a temperature at which the particles of the comminuted glass become soft and are joined to each other by mere contact, the last mentioned temperature being within the first mentioned range of temperatures, interrupting the heating when the gas developed within the glassy mass increases the volume thereof to the desired extent whereby cells are formed which are separated one from the other, and then cooling said mass, whereby multicellular glass of predetermined apparent density is produced. 4. The process for the manufacture of multicellular glass, which comprises mixing comminuted fritted vitrifiable substances with at least one pulverized substance capable'of chemically reacting with said vitrifirble substances within a certain range of temperatures, a gas being produced in the course of said reaction, heating the mixture to a temperature at which the particles of the vitriflable substances become soft and are joined to each other by mere contact, the last mentioned temperature being within the first-mentioned range of temperatures, the heating being continued until the mixture is vitrified, interrupting the heating when the gases developed within the vitrified massincr'ease the volume thereof to the desired extent whereby cells are formed which are separated one from the other, and then cooling sa'id mass, whereby multicellular glass of predetermined apparent density is produced.
5. The process for the manufacture of multicellul'ar glass, which comprises mixing a comminuted vitreous substance with pulverized substances capable of reacting with each other within a certain range of temperatures and of developing a gas in the course of this reaction, heating the mixture to a temperature at which the particles of the comminuted vitreous substance become soft and are joined to each other by mere contact, the last-mentioned temperature being within the first mentioned range of tempera-' tures, interrupting the heating when the gas developed within the vitreous massincreases the volume thereof to the desired extent whereby cells are formed which are separated one from the other, and then cooling'said mass, whereby multicellular glass of predetermined apparent density is produced.
6. The process for the manufacture of multicellular glass, which comprises 'mixing a solid comminuted vitreous substance with a pulverized substance capable of giving up a gaseous fluid within a certain range of temperatures, heating the mixture to a temperature at which the particles of the comminuted vitreous substance become soft and are joined to each other by mere contact. the last-mentioned temperature being within the first-mentioned range of temperatures, interrupting the heating when the gaseous fluid developed within the vitreous mass increases the volume thereof to the desired extent whereby cells are formed whichare separated one from the other, andthen cooling said mass, whereby multicellular glass of predetermined apparent density is produced. I
' 'l. The process of manufacturing multicellular amazes glass, which comprises mixing comminuted glass containing alkaline sulphates with a. reducing substance capable of reacting with said glass lular glass of predetermined apparent densityis produced.
8. The process of manufacturing multicellular glass, whichcomprises mixing comminuted glass ccntaining alkaline earth sulphates with a reducing substance capable of reacting with said glass within a certain range of temperatures, at least one gas being produced in the course of this reaction, heating the mixture to the softening temperature of said glass,said softening tempera.-
.ture being within said range of temperatures,
interrupting the heating when the bubbles of said gas within the glassy mass increase the volume thereof to the desired extent whereby cells are formed which are separatedone from the other, and then cooling said mass, whereby multicellular glass of predetermined apparent density is produced.
9. The process of manufacturing multicellular glass, which comprises mixing a comminuted vitreous substance containing a sulphate with a carbonaceous reducing substance capable of reacting with said vitreous substance within a certain range of temperatures, at least one gas being produced'in the course of this reaction, heating the mixture to the softening temperature of said vitreous substance, said softening temperature being within said range of temperatures, interrupting the heating when the bubbles of said gas within the vitreous mass increase the volume thereof to the desired extent wherebycells are formed which are separated one from the other, and thencooling said mass, whereby multicelluiar glass of predetermined apparent density is produced.
)0. The process of manufacturing multiceliular glass, which comprises mixing a comminuted vitreous substance with a carbonaceous reducing substance capable of reacting with said vitreous substance within a certain range of temperatures, at least one gas being produced in the course of this reaction, heating the mixture to the softening temperature of said vitreous sub stance, said softening temperature being within said range of temperatures, interrupting the heating when the bubbles of said gas within the vitreous mass increase the volume thereof to the desired extent whereby cells-are formed" which are separated one fromthe other, and then cooling said mass, whereby multicellular glass of predetermined apparent density is produced.
11. The process of manufacturing multicelluiar glass, which comprises mixing a comminuted vitreous substance with a mixture containing finely pulverized silica, soda sulphate and coal, heating the mixture to the softening temperature of said vitreous substance, said softening temperature being within the range of temperatures at which the mixture develops gas, interrupting the heating when the bubbles of said gas" within the vitreous mass increase the volume thereof to the desired extent whereby cells are formed which are separated one from the other, and then cooling said mass, whereby multicellular glass of predetermined apparent density is produced.
12. The'process of manufacturing multicellular glass, which comprises mixing a solid comminuted vitreous substance with pulverized coal, projecting this mixture into a mold heated to the range of temperatures at which the particles.
of the comminuted glass are joined to each other by mere contact, and at which gasis developed by coal, interrupting the heating when the bubbles of said'gas within the vitreous mass increase the volume thereof to the desired extent whereby cells are formed which are separated one from the other, and then cooling said mass, whereby multicellular glass of predetermined apparent density is produced.
' BERNARD LONG.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR634405X | 1934-05-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
US2123536A true US2123536A (en) | 1938-07-12 |
Family
ID=8993560
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US23709A Expired - Lifetime US2123536A (en) | 1934-05-28 | 1935-05-27 | Process for the manufacture of multicellular glass |
Country Status (5)
Country | Link |
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US (1) | US2123536A (en) |
BE (1) | BE409646A (en) |
DE (1) | DE634405C (en) |
FR (2) | FR786818A (en) |
GB (2) | GB447805A (en) |
Cited By (27)
Publication number | Priority date | Publication date | Assignee | Title |
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US2460977A (en) * | 1945-08-29 | 1949-02-08 | Minnesota Mining & Mfg | Carbon powder method of making glass beads |
US2461011A (en) * | 1945-08-29 | 1949-02-08 | Minnesota Mining & Mfg | Carbon powder method of making glass beads |
US2544954A (en) * | 1945-03-31 | 1951-03-13 | Pittsburgh Corning Corp | Preparation of cellular glass |
US2582852A (en) * | 1948-06-16 | 1952-01-15 | Pittsburgh Corning Corp | Method of making cellular glass of light color |
US2596669A (en) * | 1947-03-12 | 1952-05-13 | Pittsburgh Corning Corp | Process for making fortified cellular glass |
US2600525A (en) * | 1947-03-12 | 1952-06-17 | Pittsburgh Corning Corp | Cellular glass of increased durability |
US2691248A (en) * | 1950-12-19 | 1954-10-12 | Pittsburgh Corning Corp | Nodulated cellular glass and method of forming |
US2736142A (en) * | 1953-06-03 | 1956-02-28 | Pittsburgh Corning Corp | Process for manufacturing cellulated material |
US2773111A (en) * | 1948-01-23 | 1956-12-04 | Saint Gobain | Method and apparatus for manufacturing glass |
US2775524A (en) * | 1952-03-21 | 1956-12-25 | Pittsburgh Corning Corp | Method of producing cellulated articles |
US2837873A (en) * | 1955-03-31 | 1958-06-10 | Pittsburgh Corning Corp | Method of making dense-face, cellular vitreous bodies |
US2948034A (en) * | 1953-12-18 | 1960-08-09 | Sulzer Ag | Casting mold and method of casting carbon-containing alloys |
US2956891A (en) * | 1959-03-09 | 1960-10-18 | Armstrong Cork Co | Method of making porous products from volcanic glass and alumina |
US3174870A (en) * | 1961-12-26 | 1965-03-23 | Corning Glass Works | Foamed cellular body and method of production |
US3207588A (en) * | 1962-03-16 | 1965-09-21 | Owens Corning Fiberglass Corp | Glass foam |
US3207258A (en) * | 1964-03-17 | 1965-09-21 | Pittsburgh Corning Corp | Sound absorbing systems |
US3348933A (en) * | 1964-04-29 | 1967-10-24 | Schaumglaswerk Taubenbach Veb | Method for making foam galss |
US3361550A (en) * | 1963-12-18 | 1968-01-02 | Pilkington Brothers Ltd | Manufacture of cellular material on a molten metal bath |
US3362805A (en) * | 1965-04-21 | 1968-01-09 | Schaumglaswerk Taubenbach Veb | Production of foam glass |
US3942990A (en) * | 1972-07-13 | 1976-03-09 | Euroc Administration Ab | Method for producing foamed ceramics |
US3993495A (en) * | 1974-07-29 | 1976-11-23 | Interpace Corporation | Porous ceramic articles and method for making same |
US4081259A (en) * | 1976-09-23 | 1978-03-28 | Maryland Environmental Service | Method for forming coated cellular glass pellets |
WO1983001441A1 (en) * | 1981-10-14 | 1983-04-28 | Buarque De Macedo, Pedro, Manoel | Method and composition for making foam glass from diatomaceous earth and fly ash |
US4632876A (en) * | 1985-06-12 | 1986-12-30 | Minnesota Mining And Manufacturing Company | Ceramic spheroids having low density and high crush resistance |
US4725390A (en) * | 1985-06-12 | 1988-02-16 | Minnesota Mining And Manufacturing Company | Process for making ceramic spheroids |
US6988378B1 (en) * | 2000-07-27 | 2006-01-24 | Corning Incorporated | Light weight porous structure |
US8991213B1 (en) | 2010-07-22 | 2015-03-31 | Biome International, Inc. | Method for producing cellular glass from waste glass streams |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2514324A (en) * | 1945-04-24 | 1950-07-04 | Pittsburgh Corning Corp | Preparation of cellulated glass bodies |
US2485724A (en) * | 1945-12-21 | 1949-10-25 | Pittsburgh Corning Corp | Method of making lightweight cellular materials |
US2611712A (en) * | 1949-01-12 | 1952-09-23 | Pittsburgh Corning Corp | Method of preparing a cellulated glass body |
FR2202046B1 (en) * | 1972-10-09 | 1976-10-29 | Saint Gobain | |
CH637097A5 (en) * | 1978-06-21 | 1983-07-15 | Foerderung Forschung Gmbh | Method for producing foam glass and then made foam glass. |
DE102014003258B4 (en) | 2014-03-12 | 2020-12-03 | Calsitherm Verwaltungs Gmbh | Solar energy collector and molding device for the production of foam glass bodies |
DE102015204752A1 (en) | 2015-03-17 | 2016-09-22 | Schaeffler Technologies AG & Co. KG | Method for producing a porous component from at least one material M and having a foam structure and a porous component produced thereafter |
-
0
- BE BE409646D patent/BE409646A/xx unknown
-
1934
- 1934-05-28 FR FR786818D patent/FR786818A/en not_active Expired
-
1935
- 1935-01-08 DE DES116690D patent/DE634405C/en not_active Expired
- 1935-05-27 US US23709A patent/US2123536A/en not_active Expired - Lifetime
- 1935-05-28 GB GB15534/35A patent/GB447805A/en not_active Expired
- 1935-05-28 GB GB31784/35A patent/GB447821A/en not_active Expired
- 1935-06-15 FR FR46886D patent/FR46886E/en not_active Expired
Cited By (28)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2544954A (en) * | 1945-03-31 | 1951-03-13 | Pittsburgh Corning Corp | Preparation of cellular glass |
US2461011A (en) * | 1945-08-29 | 1949-02-08 | Minnesota Mining & Mfg | Carbon powder method of making glass beads |
US2460977A (en) * | 1945-08-29 | 1949-02-08 | Minnesota Mining & Mfg | Carbon powder method of making glass beads |
US2596669A (en) * | 1947-03-12 | 1952-05-13 | Pittsburgh Corning Corp | Process for making fortified cellular glass |
US2600525A (en) * | 1947-03-12 | 1952-06-17 | Pittsburgh Corning Corp | Cellular glass of increased durability |
US2773111A (en) * | 1948-01-23 | 1956-12-04 | Saint Gobain | Method and apparatus for manufacturing glass |
US2582852A (en) * | 1948-06-16 | 1952-01-15 | Pittsburgh Corning Corp | Method of making cellular glass of light color |
US2691248A (en) * | 1950-12-19 | 1954-10-12 | Pittsburgh Corning Corp | Nodulated cellular glass and method of forming |
US2775524A (en) * | 1952-03-21 | 1956-12-25 | Pittsburgh Corning Corp | Method of producing cellulated articles |
US2736142A (en) * | 1953-06-03 | 1956-02-28 | Pittsburgh Corning Corp | Process for manufacturing cellulated material |
US2948034A (en) * | 1953-12-18 | 1960-08-09 | Sulzer Ag | Casting mold and method of casting carbon-containing alloys |
US2837873A (en) * | 1955-03-31 | 1958-06-10 | Pittsburgh Corning Corp | Method of making dense-face, cellular vitreous bodies |
US2956891A (en) * | 1959-03-09 | 1960-10-18 | Armstrong Cork Co | Method of making porous products from volcanic glass and alumina |
US3174870A (en) * | 1961-12-26 | 1965-03-23 | Corning Glass Works | Foamed cellular body and method of production |
US3207588A (en) * | 1962-03-16 | 1965-09-21 | Owens Corning Fiberglass Corp | Glass foam |
US3361550A (en) * | 1963-12-18 | 1968-01-02 | Pilkington Brothers Ltd | Manufacture of cellular material on a molten metal bath |
US3207258A (en) * | 1964-03-17 | 1965-09-21 | Pittsburgh Corning Corp | Sound absorbing systems |
US3348933A (en) * | 1964-04-29 | 1967-10-24 | Schaumglaswerk Taubenbach Veb | Method for making foam galss |
US3362805A (en) * | 1965-04-21 | 1968-01-09 | Schaumglaswerk Taubenbach Veb | Production of foam glass |
US3942990A (en) * | 1972-07-13 | 1976-03-09 | Euroc Administration Ab | Method for producing foamed ceramics |
US3993495A (en) * | 1974-07-29 | 1976-11-23 | Interpace Corporation | Porous ceramic articles and method for making same |
US4081259A (en) * | 1976-09-23 | 1978-03-28 | Maryland Environmental Service | Method for forming coated cellular glass pellets |
WO1983001441A1 (en) * | 1981-10-14 | 1983-04-28 | Buarque De Macedo, Pedro, Manoel | Method and composition for making foam glass from diatomaceous earth and fly ash |
US4632876A (en) * | 1985-06-12 | 1986-12-30 | Minnesota Mining And Manufacturing Company | Ceramic spheroids having low density and high crush resistance |
US4725390A (en) * | 1985-06-12 | 1988-02-16 | Minnesota Mining And Manufacturing Company | Process for making ceramic spheroids |
AU584207B2 (en) * | 1985-06-12 | 1989-05-18 | Minnesota Mining And Manufacturing Company | Ceramic spheroids having low density and high crush resistance |
US6988378B1 (en) * | 2000-07-27 | 2006-01-24 | Corning Incorporated | Light weight porous structure |
US8991213B1 (en) | 2010-07-22 | 2015-03-31 | Biome International, Inc. | Method for producing cellular glass from waste glass streams |
Also Published As
Publication number | Publication date |
---|---|
FR46886E (en) | 1936-10-30 |
GB447805A (en) | 1936-05-26 |
BE409646A (en) | |
DE634405C (en) | 1936-08-27 |
FR786818A (en) | 1935-09-10 |
GB447821A (en) | 1936-05-26 |
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